EP0294168A1 - Procédé de préparation d'un polymère à base d'éthylène - Google Patents

Procédé de préparation d'un polymère à base d'éthylène Download PDF

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Publication number
EP0294168A1
EP0294168A1 EP88304983A EP88304983A EP0294168A1 EP 0294168 A1 EP0294168 A1 EP 0294168A1 EP 88304983 A EP88304983 A EP 88304983A EP 88304983 A EP88304983 A EP 88304983A EP 0294168 A1 EP0294168 A1 EP 0294168A1
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Prior art keywords
ethylene
magnesium
titanium
based polymer
producing
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EP88304983A
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German (de)
English (en)
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EP0294168B1 (fr
Inventor
Kenji Nakacho
Norio Tomotsu
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Idemitsu Petrochemical Co Ltd
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Idemitsu Petrochemical Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond

Definitions

  • the present invention relates to a method for producing an ethylene-based polymer. More particularly, the invention relates to a method for producing an ethylene-based polymer having properties suitable for use as a material of blow-­molded articles and films by polymerizing ethylene or a monomer mixture mainly composed of ethylene in the presence of a highly active Ziegler-type catalyst system prepared in a specific procedure.
  • polyolefins can be produced by polymerizing olefins by use of a solid catalyst system composed of a reaction product of an organic magnesium compound, organic titanium compound, zirconium compound and aluminum halide and an organometallic compound (see, for example, Japanese Patent Publication 55-8083 and Japanese Patent Kokai 56-151704 and 52-39714).
  • a solid catalyst system composed of a reaction product of an organic magnesium compound, organic titanium compound, zirconium compound and aluminum halide and an organometallic compound.
  • the present invention accordingly has an object to provide a novel method for producing an ethylene-based polymer by use of a specifically prepared catalyst system having a greatly enhanced catalytic activity over conven­tional catalyst systems, in which the molecular weight distribution of the polymer product can be controlled in a wide range to satisfy the particular requirements for the properties of the polymer in accordance with the intended application thereof.
  • the most characteristic feature of the inventive method consists in the specific procedure for the preparation of the catalyst system which belongs to a type of so-called Ziegler catalysts.
  • the method of the present invention for producing an ethylene-based polymer comprises polymerizing ethylene or a monomer mixture mainly composed of ethylene in the presence of a catalyst system comprising:
  • the most important feature of the inventive method consists in the process for the preparation of the catalyst system or, in particular, the solid catalytic ingredient i.e. cata­lytic ingredient (A), as one of the constituents of the catalyst system.
  • the first step, i.e. step (a), in the process for the preparation of the catalytic ingredient (A) is performed by bringing a mixture of a magnesium dialkoxide of the general formula Mg(OR1)2 and a tetraalkoxide of titanium or zirconium of the general formula M1(OR2)4 into contact with an alkanol of the general formula R3OH to prepare a magnesium-containing solid complex.
  • the monovalent hydrocarbon group denoted by R1 in the general formula representing the magnesium alkoxide has 1 to 20 carbon atoms or, preferably, 1 to 8 carbon atoms and may be aliphatic, alicyclic or aromatic.
  • suitable magnesium dialkoxide include magnesium dimethoxide, magnesium diethoxide, magnesium dipropoxide, magnesium diisopropoxide, magnesium diallyloxide, magnesium di-n-­butoxide, magnesium di-sec-butoxide, magnesium diisobutox­ide, magnesium di-tert-butoxide, magnesium dibutenoxide, magnesium dipentoxide, magnesium dioctoxide, magnesium dicyclopentoxide, magnesium diphenoxide, magnesium diben­zyloxide, magnesium methoxide ethoxide, magnesium methoxide propoxide, magnesium ethoxide propoxide and the like, of which magnesium dimethoxide, magnesium diethoxide and magnesium dipropoxide are preferable or magnesium diethoxide is more preferable.
  • magnesium dialkoxide or dialkoxides is essential as the magnesium source in the preparation of the catalytic ingredient (A) of the catalyst system used in the inventive method.
  • a magnesium source material other than the dialkoxides such as metallic magnesium, alkylmagnesium halides and the like, with a tetraalkoxide of titanium or zirconium leading to a poor morphology of the resultant polymer product.
  • the tetraalkoxide of titanium or zirconium used in combination with the above described magnesium dialkoxide is represented by the general formula M1 (OR2)4, in which M1 is an atom of titanium or zirconium and R2 is a monovalent hydrocarbon group having 1 to 20 carbon atoms selected from the class consisting of alkyl groups, cycloalkyl groups, aryl groups and aralkyl groups.
  • titanium and zirconium tetraalkoxides include tetramethoxy titanium, tetraethoxy titanium, tetra(n-propoxy) titanium, tetra(n-butoxy) titanium, tetra(n-pentoxy) titanium, tetra­(n-hexoxy) titanium, tetra(n-heptoxy ⁇ titanium, tetra(n-­octoxy) titanium, tetracyclopentoxy titanium, tetracyclo­hexoxy titanium, tetracycloheptoxy titanium, tetracyclo­octoxy titanium, tetraphenoxy titanium and the like as well as zirconium compounds corresponding to the above named titanium compounds by replacing the titanium atom with a zirconium atom.
  • titanium or zirconium tetraalkoxide cannot be replaced with other titanium or zirconium compounds such as titanium halides, alkoxytitanium halides, zirconium halides, alkoxyzirconium halides and the like since these titanium or zirconium compounds are poorly compatible with the magnesium dialkoxide and only with difficulty give a uniform mixture.
  • the magnesium dialkoxide and the titanium or zirconium tetraalkoxide are mixed together at a temperature in the range from room temperature to 150 °C into a uniform mixture in a molar ratio of 1:0.4 to 1:5 or, preferably, 1:0.5 to 1:2.
  • the mixture of the magnesium dialkoxide and the titanium or zirconium tetraalkoxide is brought into contact with an alkanol represented by the general formula R3OH, in which R3 is an alkyl group having 1 to 5 carbon atoms.
  • R3 is an alkyl group having 1 to 5 carbon atoms.
  • Isopropyl alcohol is particularly preferable as the alkanol.
  • the amount of the alkanol is usually in the range from 1 to 100 moles or, preferably, from 2 to 50 moles per mole of the magnesium dialkoxide.
  • the mixture of the magnesium dialkoxide and titanium or zirconium tetraalkoxide When the mixture of the magnesium dialkoxide and titanium or zirconium tetraalkoxide is brought into contact with the alkanol, a solid complex is precipitated in the mixture, of which the main constituent is the magnesium dialkoxide containing titanium or zirconium.
  • the thus obtained solid complex has a specific surface area of usually, at least 30 m2/g or, in most cases, 80 to 200 m2/g, which is much larger than that of conventional magnesium dialkoxide available on the market.
  • step (b) of the process is a reaction of the above obtained magnesium-containing solid complex with a zirconium tetraalkoxide, zirconium tetra­halide, e.g., zirconium tetrachloride, tetrabromide and tetraiodide, or a combination thereof, when the tetra­alkoxide used in step (a) is a titanium tetraalkoxide, or with a titanium tetraalkoxide, titanium tetrahalide, e.g., titanium tetrachloride, tetrabromide and tetraiodide, or a combination thereof, when the tetraalkoxide used in step (a) is a zirconium tetraalkoxide.
  • a zirconium tetraalkoxide zirconium tetraalkoxide
  • zirconium tetraalkoxide zi
  • Examples of the zirconium or titanium tetraalkoxide used in step (b) may be the same ones as named before as the examples of the tetraalkoxide used in step (a).
  • the zirconium or titanium tetraalkoxide can be replaced with or may be combined with a zirconium or titanium tetrahalide, respectively.
  • the amount of the zirconium or titanium tetraalkoxide and/or tetrahalide to be reacted in step (b) with the magnesium-containing solid complex obtained in step (a) is usually in the range from 0.01 to 2 moles or, preferably, from 0.05 to 1 mole per mole of the magnesium content in the magnesium-containing solid complex.
  • halogenation treat it is optional according to need to undertake a halogenation treatment of the magnesium-containing solid complex prior to the reaction with the zirconium or titanium tetraalkoxide and/or tetrahalide.
  • the halogenation treat­ment gives advantages to prevent formation of coarse agglo­merates of the catalyst particles and to prevent adhesive deposition of the catalyst particles on to the walls of the reactor in which the catalyst is prepared.
  • the halogenation treatment or, typically, chlorination treatment of the solid complex can be performed by directly contacting the solid complex as such with a chlorinating agent at a temperature in the range from 0 to 100 °C but the uniformity of the chlorination can be increased when the chlorination reaction is performed by dispersing the solid complex in a suitable inert solvent.
  • Suitable halogenating agents include elementary halo­gens, thionyl halides, silicon tetrahalides and anhydrous hydrogen halides, the halogen being chlorine, fluorine or bromine.
  • the amount of the halogenating agent to be used should be sufficient to provide at least 0.1 mole or, preferably, from 0.2 to 100 moles of the halogen atoms per mole of the magnesium atoms contained in the magnesium-­containing solid complex.
  • the reaction product obtained in step (b) should contain zirconium and titanium in a molar ratio Zr:Ti of 0.2:1 to 20:1 or, preferably, 0.5:1 to 10:1.
  • step (c) of the process the reaction product obtained in the above described step (b) is then reacted with an organoaluminum halide compound to give the catalytic ingredient (A) in the catalyst system used in the inventive method.
  • the organoaluminum halide used here is represented by the general formula AlR5 n X 3-n , in which R5 is an alkyl group having 1 to 20 carbon atoms, X is an atom of halogen, such as chlorine and bromine, and the subscript n is 1 or 2.
  • organoaluminum halide examples include dimethyl­aluminum monochloride and monobromide, diethylaluminum monochloride and monobromide, diisopropylaluminum mono­chloride and monobromide, diisobutylaluminum monochloride and monobromide, methylaluminum dichloride and dibromide, ethylaluminum dichloride and dibromide isopropylaluminum dichloride and dibromide, isobutylaluminum dichloride and dibromide and the like.
  • organoaluminum halides can be used either singly or as a combination of two kinds or more according to need.
  • reaction of the reaction product obtained in step (b) and the organoaluminum halide in step (c) has an effect to enhance the bonding strength between the titanium or zirconium compound and the magnesium-­containing solid complex as a carrier thereof.
  • step (c) described above can be used as such as the catalytic ingre­dient (A) in the catalyst system used in the inventive method, it is optional that the solid product is again reacted with the titanium compound and/or zirconium compound followed by a second reaction with the organoaluminum halide.
  • the catalytic ingredient (A) obtained in the above described manner should contain from 0.1 to 100 moles or, preferably, from 0.5 to 40 moles of the organoaluminum halide per mole of the content of magnesium.
  • the molar ratio of zirconium to titanium, Zr:Ti, in the catalytic ingredient (A) should be in the range from 0.5:1 to 20:1 or, preferably, from 1:1 to 10:1.
  • Zr:Ti molar ratio is smaller than 0.5, the molecular weight distribution of the resultant ethylene-based polymer would be too narrow.
  • this molar ratio exceeds 20, on the other hand, the catalyst system with the catalytic ingredient (A) combined with the catalytic ingredient (B) would have a somewhat decreased catalytic activity.
  • the catalytic ingredient (A) described above is used in combination with an organoaluminum compound as the cata­lytic ingredient (B) to form the catalyst system used in the inventive method.
  • organoaluminum compounds can be used as the catalytic ingredient (B) without par­ticular limitations.
  • a preferable class of the organo­aluminum compound include those represented by the general formulas R3Al, R2AlX, R3Al2X2 and R2AlOR′, in which R and R′ are each an alkyl group or aryl group having 1 to 8 carbon atoms and X is an atom of halogen such as chlorine and bromine.
  • organoaluminum compounds include trimethyl aluminum, triethyl aluminum, triisopropyl alumi­num, triisobutyl aluminum, diethyl aluminum monochloride, diisopropyl aluminum monochloride, diisobutyl aluminum mono­chloride, diethyl aluminum monomethoxide, dimethyl aluminum monoethoxide, diethyl aluminum monobutoxide, diethyl alumi­num phenoxide, ethyl aluminum dichloride, isopropyl aluminum dichloride, methyl aluminum sesquichloride, ethyl aluminum sesquichloride and the like, of which diethyl aluminum mono­chloride, triethyl aluminum and triisobutyl aluminum are preferred.
  • organoaluminum compounds can be used either singly or as a combination of two kinds or more according to need. Further, it is optional to use an alkyl-­containing aluminoxane obtained by the reaction of an alkyl aluminum and water as the catalytic ingredient (B).
  • the amount of the catalytic ingredient (B) to be combined with the catalytic ingredient A) is in the range from 1 to 1000 moles or, preferably, from 10 to 200 moles as aluminum per mole of the overall amount of titanium and zirconium in the catalytic ingredient (A).
  • the catalystic ingredients (A) and (B) are added to an inert solvent such as a hydrocabron solvent and the monomer or monomer mixture is introduced into the mixture kept at a temperature in the range from 20 to 200 °C under a pressure in the range from 1 to 200 kg/cm2. Bulk polymer­ization and gas-phase polymerization can also be performed.
  • the polymerization reaction can be performed as a batch-wise process or as a continuous process.
  • the average molecular weight of the ethylene-based polymer as a product of the inventive method can be con­trolled by any conventional method including addition of hydrogen into the monomer or by means of control of the polymerization temperature and catalyst concentration as well as modification of the catalyst composition.
  • the catalyst system used in the inventive method is highly active so that a great cost saving can be obtained by omitting the expensive treat­ment of the polyethylene product for the removal of the catalyst residue.
  • the catalyst system is highly durable so that polymer products having excellent morphology can be obtained.
  • the products of ethylene-based polymer obtained by the inventive method have a relatively wide molecular weight distribution so that the polymer is suitable as a material for blow molding of hollow articles and inflation method for the manufacture of films.
  • the polymer products in the examples were evaluated in terms of the melt index MI 2.16 determined at 190 °C under a load of 2.16 kg according to the procedure specified in JIS and of the flow ratio F.R. as a measure of the molecular weight distribution, which is a ratio of the melt index MI 21.6 determined at 190 °C under a load of 21.6 kg to the MI 2.16 .
  • the solution was added dropwise to 120 ml of isopropyl alcohol kept at 20 °C under agitation over a period of 1 hour followed by further continued agitation for additional 1 hour so that a solid material was precipitated in the mixture.
  • the precipitates were washed repeatedly with anhydrous hexane until titanium could no longer be detected in the washings.
  • the thus obtained magnesium-containing solid complex had a specific surface area of 130 m2/g and the content of titanium therein was 0.62% by weight.
  • An autoclave of 1 liter capacity equipped with a stirrer was charged with 400 ml of hexane and heated at 80 °C. After thoroughly replacing the atmospheric gas inside the autoclave with hydrogen, hydrogen was compressed into the autoclave up to a pressure of 1.9 kg/cm2G and then ethylene was introduced thereinto up to a total pressure of 4.4 kg/cm2G.
  • the table below gives the contents of titanium and zirconium in the catalytic ingredient (A) prepared in step [2], the partial pressures of ethylene and hydrogen in step [3], the activity of the catalyst system as expressed by the yield of polyethylene obtained by the polymerization reaction for 1 hour per gram of the titanium and zirconium in the catalyst system and the MI 2.16 and F.R. for the characterization of the polyethylene product.
  • the experimental procedure was substantially the same as in Example 1 except that the amount of the titanium tetra(n-butoxide) used in step [2] was decreased to 2 m moles instead of 6 m moles. Relevant data are shown in the table.
  • Example 2 The experimental procedure was substantially the same as in Example 1 except that the titanium tetra(n-butoxide) used in step [2] of Example 1 was omitted. Relevant data are shown in the table.
  • Example 2 The experimental procedure was substantially the same as in Example 1 except that 56 m moles of the titanium tetra(n-butoxide) used in step [1] of Example 1 were replaced with 56 m moles of zirconium tetra(n-butoxide) and the zirconium tetra(n-butoxide) used in step [2] was omitted. Relevant data are shown in the table.
  • a solution prepared by dissolving 4.5 g (12 m moles) of zirconium tetra(n-butoxide) in 50 ml of hexane was added dropwise into the slurry of the magnesium-containing solid complex kept at 20 °C with agitation over a period of 15 minutes followed by heating of the mixture under reflux for 90 minutes to effect the reaction. Thereafter, 102 ml of a 50% by weight hexane solution of ethyl aluminum dichloride C2H5AlCl2 were added dropwise into the mixture kept at 20 °C under agitation over a period of 30 minutes followed by heating of the mixture under reflux for 60 minutes to effect the reaction.
  • the solid material in the mixture was washed repeatedly with anhydrous hexane until chlorine could no longer be detected in the washings and then hexane was added to the mixture to make up an overall volume of 500 ml. Then, a solution of 2.0 g (6 m moles) of titanium tetra(n-­butoxide) dissolved in 50 ml of hexane was added dropwise into the mixture kept at 20 °C over a period of 15 minutes followed by further continued agitation for additional 1 hour.
  • the polymerization was conducted in substantially the same manner as in step [3] of Example 1 excepting the use of the solid material obtained in [2] above as the catalytic ingredient (A). Relevant data are shown in the table.
  • Example 5 The experimental procedure was substantially the same as in Example 5 excepting replacement of 2.0 g (6 m moles) of titanium tetra(n-butoxide) used in step [2] of Example 5 with 0.67 ml (6 m moles) of titanium tetrachloride. Relevant data are shown in the table.
  • the experimental procedure was substantially the same as in Example 1 except that the amount of the aluminum triisobutoxide used in step [3] was decreased to 0.24 m mole and the partial pressures of ethylene and hydrogen were 2.5 kg/cm2 and 3.0 kg/cm2, respectively. Relevant data are shown in the table.
  • Example 7 The experimental procedure was substantially the same as in Example 7 except that 0.24 m mole of aluminum triisobutoxide was replaced with a combination of 0.12 m mole of aluminum triisobutoxide and 0.12 m mole of diethyl aluminum monochloride. Relevant data are shown in the table.
  • a mixture prepared by adding 3.7 g (22 m moles) of silicon tetrachloride to a dispersion of 10 g of magnesium diethoxide in 200 ml of hexane was agitated at 20 °C and 1.5 g (33 m moles) of ethyl alcohol were added thereto dropwise over a period of 1 hour followed by heating of the mixture under reflux for 2 hours to effect the reaction.
  • the magnesium-containing solid material produced in the mixture was washed repeatedly with anhydrous hexane until ethyl alcohol could no longer be detected in the washings followed by the addition of hexane to make up an overall volume of 500 ml.
  • step [1] The procedures subsequent to step [1] above were sub­stantially the same as in [2] and [3] of Example 1 excepting the use of the magnesium-containing carrier obtained in step [1] above in place of the magnesium-containing solid complex prepared in step [1] of Example 1. Relevant data are shown in the table.
  • the experimental procedure was substantially the same as in Comparative Example 1 excepting omission of the chlo­rination reaction by adding silicon tetrachloride in the preparation of the magnesium-containing carrier. Relevant data are shown in the table.
  • a slurry of the magnesium-containing solid material obtained in the same procedure as in step [1] of Example 1 was admixed with 4.9 ml of silicon tetraethoxide and 25 ml of titanium tetrachloride and the mixture was heated under reflux for 60 minutes to effect the reaction.
  • the solid material in the mixture was washed repeatedly with hexane until chlorine could no longer be detected in the washings.
  • the magnesium-containing solid complex obtained in step [1] was admixed with hexane to make up a volume of 500 ml and the mixture was admixed with 3.7 g (22 m moles) of silicon tetrachloride followed by dropwise addition of 1.5 g (33 m moles) of ethyl alcohol at 20 °C with agitation over a period of 1 hour and heating under reflux for 2 hours to effect the reaction.
  • the thus obtained magnesium-con­taining solid material was washed repeatedly with anhydrous hexane until ethyl alcohol could no longer be detected in the washings. Relevant data are shown in the table.
  • the experimental procedure was substantially the same as in Example 1 except that 0.3 g of butene-1 was added to the autoclave as a comonomer to be copolymerized with ethylene and the autoclave was first pressurized with hydrogen up to a pressure of 1.9 kg/cm2G and then with ethylene up to a pressure of 4.4 kg/cm2G. Relevant data are shown in the table.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
EP19880304983 1987-06-02 1988-06-01 Procédé de préparation d'un polymère à base d'éthylène Expired EP0294168B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP137712/87 1987-06-02
JP62137712A JPH0725827B2 (ja) 1987-06-02 1987-06-02 エチレン重合体の製造方法

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EP0294168A1 true EP0294168A1 (fr) 1988-12-07
EP0294168B1 EP0294168B1 (fr) 1991-11-13

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CA (1) CA1304882C (fr)
DE (1) DE3866166D1 (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0448115A2 (fr) * 1990-03-23 1991-09-25 Tosoh Corporation Procédé de production d'une polyoléfine
EP0574067A1 (fr) * 1992-06-09 1993-12-15 SOLVAY (Société Anonyme) Procédé de fabrication d'un solide catalytique, solide catalytique et procédé de (co)polymérisation d'oléfines au moyen de ce solide catalytique
WO1994000498A1 (fr) * 1992-06-22 1994-01-06 Borealis Holding A/S Procede de preparation d'une composition de procatalyse par impregnation d'un support avec un alcoxyde de magnesium, un alcoxyde de titane et une solution d'alcool
US5494982A (en) * 1989-05-19 1996-02-27 Idemitsu Petrochemical Company, Limited Process for preparing ethylenic polymer composition
US5629390A (en) * 1990-03-23 1997-05-13 Tosoh Corporation Method for producing a polyolefin
US6054406A (en) * 1989-10-18 2000-04-25 Montell North America Inc. Polymetallic catalysts and method of preparing same
US6759362B2 (en) 1999-06-30 2004-07-06 Union Carbide Chemicals & Plastics Technology Corporation Mixed metal alkoxide complexes and polymerization catalysts made therefrom

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2307824A1 (fr) * 1975-04-14 1976-11-12 Solvay Procede pour la polymerisation des olefines
EP0043473A1 (fr) * 1980-06-25 1982-01-13 Idemitsu Kosan Company Limited Procédé de préparation de polyéthylène

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5141174A (ja) * 1974-10-05 1976-04-06 Mitsubishi Petrochemical Co Makitotsutaobijotainotorihazushihoho oyobi sochi
JPS56151704A (en) * 1980-04-25 1981-11-24 Shindaikiyouwa Sekiyu Kagaku Kk Preparation of polyolefin

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2307824A1 (fr) * 1975-04-14 1976-11-12 Solvay Procede pour la polymerisation des olefines
EP0043473A1 (fr) * 1980-06-25 1982-01-13 Idemitsu Kosan Company Limited Procédé de préparation de polyéthylène

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5494982A (en) * 1989-05-19 1996-02-27 Idemitsu Petrochemical Company, Limited Process for preparing ethylenic polymer composition
US6054406A (en) * 1989-10-18 2000-04-25 Montell North America Inc. Polymetallic catalysts and method of preparing same
US6433119B1 (en) 1989-10-18 2002-08-13 Basell Poliolefine Italia S.P.A. Polymetallic catalysts, method of preparing and polymers produced thereby
EP0448115A2 (fr) * 1990-03-23 1991-09-25 Tosoh Corporation Procédé de production d'une polyoléfine
EP0448115A3 (en) * 1990-03-23 1992-04-01 Tosoh Corporation Method for producing a polyolefin
US5629390A (en) * 1990-03-23 1997-05-13 Tosoh Corporation Method for producing a polyolefin
EP0574067A1 (fr) * 1992-06-09 1993-12-15 SOLVAY (Société Anonyme) Procédé de fabrication d'un solide catalytique, solide catalytique et procédé de (co)polymérisation d'oléfines au moyen de ce solide catalytique
BE1005982A3 (fr) * 1992-06-09 1994-04-12 Solvay Procede de fabrication d'un solide catalytique, solide catalytique et procede de (co)polymerisation d'olefines au moyen de ce solide catalytique.
US5631334A (en) * 1992-06-09 1997-05-20 Solvay (Soci et e Anonyme) Process for the manufacture of a catalytic solid, catalytic solid and process for (co)polymerisation of olefins by means of this catalytic solid
WO1994000498A1 (fr) * 1992-06-22 1994-01-06 Borealis Holding A/S Procede de preparation d'une composition de procatalyse par impregnation d'un support avec un alcoxyde de magnesium, un alcoxyde de titane et une solution d'alcool
US6759362B2 (en) 1999-06-30 2004-07-06 Union Carbide Chemicals & Plastics Technology Corporation Mixed metal alkoxide complexes and polymerization catalysts made therefrom

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DE3866166D1 (de) 1991-12-19
JPS63301209A (ja) 1988-12-08
CA1304882C (fr) 1992-07-07
EP0294168B1 (fr) 1991-11-13
JPH0725827B2 (ja) 1995-03-22

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